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SU213823A1 - - Google Patents

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Publication number
SU213823A1
SU213823A1 SU1043458A SU1043458A SU213823A1 SU 213823 A1 SU213823 A1 SU 213823A1 SU 1043458 A SU1043458 A SU 1043458A SU 1043458 A SU1043458 A SU 1043458A SU 213823 A1 SU213823 A1 SU 213823A1
Authority
SU
USSR - Soviet Union
Prior art keywords
tetrachloropropene
pentachloropropane
yield
synthesis
temperature
Prior art date
Application number
SU1043458A
Other languages
Russian (ru)
Publication of SU213823A1 publication Critical patent/SU213823A1/ru

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Изобретение относитс  к области получёни  1,1,2,3-тетрахлорПропена-1 исходного продукта дл  синтеза селективного гербицида против овсюга-диптала.The invention relates to the field of 1,1,2,3-tetrachloropropena-1 of a starting material for the synthesis of a selective herbicide against oat-diptal.

Известны методы синтеза этого хлорида на Основе товарного 1,1,1,3-тетрахлорпропена путем последовательного проведени  стадий деГидрохлорировани  и хлорировани , а также метод синтеза, заключающийс  в хлорировании 2,3-дихлорпропена газообразным хлором в присутствии азобисизобутиронитрила . При этом требуетс  очистка образующихс  токсичных сточных вод, кроме того, способ сопровождаетс  образованием побочного продукта 1,1,1,2-тетрахлорпропена-2.There are known methods for the synthesis of this chloride on the basis of commodity 1,1,1,3-tetrachloropropene by sequentially carrying out the steps of dehydrochlorination and chlorination, as well as the synthesis method consisting in chlorination of 2,3-dichloropropene with chlorine gas in the presence of azobisisobutyronitrile. This requires purification of the toxic wastewater generated, in addition, the method is accompanied by the formation of a byproduct of 1,1,1,2-tetrachloropropene-2.

Предложенный способ свободен от этих недостатков и более прост в аппаратурном оформлении.The proposed method is free from these disadvantages and more simple in hardware design.

Способ заключаетс  в дегидрохлорировании пентахлорпропана в паровой фазе над катализатором (хлористый цинк, осажденный на пористом носителе) при температуре 300-500°С с образованием конечного продукта без примесей изомерного 1,1,2,3-тетрахлорпропена-2 , выход 85%.The method consists in dehydrochlorinating pentachloropropane in the vapor phase over a catalyst (zinc chloride precipitated on a porous carrier) at a temperature of 300-500 ° C to form the final product without isomeric 1,1,2,3-tetrachloropropene-2 impurities, yield 85%.

Пример. В вертикальную трубку, снабженную электрообогревом и термопарой, помещают кусочки пемзы (около 100 мл), пропитанные насыщенным раствором хлористого цинка, и высущнвают их в токе сухого азота при температуре 200°С. Трубку нагревают до 400°С и со скоростью 0,5 мл/мин прикапывают 56 г пентахлорпропана. Выход 1,1,2,3-тетрахлорпропена-1 составл ет 42 гExample. Pumice pieces (about 100 ml) soaked in a saturated solution of zinc chloride are placed in a vertical tube equipped with electrical heating and a thermocouple, and extrude them in a stream of dry nitrogen at a temperature of 200 ° C. The tube is heated to 400 ° C and 56 g of pentachloropropane are added dropwise at a rate of 0.5 ml / min. The yield of 1,1,2,3-tetrachloropropen-1 is 42 g.

(87о/о); т. кип. 68-69°С (30 мм рт. ст); (87o / o); m.p. 68-69 ° С (30 mmHg);

1,5191.1.5191.

Предмет и з о б р е т е и «  Subject and reference to the and “

Способ получени  1,1,2,3-тетрахлорпропена-1 путем дегидрохлорировани  1,1,1,2,3-пентахлорпропана при нагревании, отличающийс  тем, что, с целью повыщени  выхода иThe method of producing 1,1,2,3-tetrachloropropen-1 by dehydrochlorinating 1,1,1,2,3-pentachloropropane with heating, characterized in that, in order to increase the yield and

улучщени  качества конечного продукта, упрощени  процесса и полного отсутстви  сточных вод, процесс дегидрохлорировани  провод т в паровой фазе при температуре 300- 500С в присутствии хлористого цинка, осажденного на пористом носителе.improving the quality of the final product, simplifying the process and the complete absence of wastewater, the dehydrochlorination process is carried out in the vapor phase at a temperature of 300-500 ° C in the presence of zinc chloride precipitated on a porous carrier.

SU1043458A SU213823A1 (en)

Related Child Applications (2)

Application Number Title Priority Date Filing Date
SU874255320A Addition SU1435923A2 (en) 1987-04-06 1987-04-06 Method of using heat of waste gases
SU874346346A Addition SU1502943A2 (en) 1987-12-21 1987-12-21 Method of regenerating waste gas heat

Publications (1)

Publication Number Publication Date
SU213823A1 true SU213823A1 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20120289751A1 (en) * 2009-11-27 2012-11-15 Masatoshi Nose Process for preparing 1,1,2,3-tetrachloropropene
WO2017053159A1 (en) 2015-09-21 2017-03-30 Arkema Inc. Process for making tetrachloropropene by catalyzed gas-phase dehydrochlorination of pentachloropropane

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20120289751A1 (en) * 2009-11-27 2012-11-15 Masatoshi Nose Process for preparing 1,1,2,3-tetrachloropropene
US8791311B2 (en) * 2009-11-27 2014-07-29 Daikin Industries, Ltd. Process for preparing 1,1,2,3-tetrachloropropene
WO2017053159A1 (en) 2015-09-21 2017-03-30 Arkema Inc. Process for making tetrachloropropene by catalyzed gas-phase dehydrochlorination of pentachloropropane

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